Effect of CTAB as a foaming agent on the properties of alumina ceramic membranes

2014 ◽  
Vol 40 (4) ◽  
pp. 5299-5305 ◽  
Author(s):  
M.F. Zawrah ◽  
R.M. Khattab ◽  
Lamey G. Girgis ◽  
E.E. El Shereefy ◽  
S.E. Abo Sawan
2014 ◽  
Vol 699 ◽  
pp. 336-341 ◽  
Author(s):  
Nurulfazielah Nasir ◽  
Ridhwan Jumaidin ◽  
Hady Efendy ◽  
Mohd Zulkefli Selamat ◽  
Goh Keat Beng ◽  
...  

Aluminium powder was used as foaming agent in the production of macro-porous alumina ceramic. The porous ceramic material was developed by mixing an appropriate composition of cement, aluminium powder (Al), alumina (Al2O3), calcium oxide (CaO), gypsum (calcium sulphate dehydrate, CaSO4.2H2O), silica powder and deionized water. Different compositions of porous ceramic were produced at 2wt.%, 3wt.% and 4wt.% of aluminium powder. Their mechanical properties and macro-porosity structural of the porous ceramic material were analysed and compared. It is determined that the optimal properties of porous ceramic material were found at 3wt.% of aluminium powder and degraded drastically at 4wt.%. This phenomenon is due to the chemical reaction between the aluminium powder and DI water in which they form aluminium oxide that promotes the strength of the material but at the same time, more pores are created at higher reaction rate between these two fundamental materials.


1988 ◽  
Vol 39 (3) ◽  
pp. 243-258 ◽  
Author(s):  
Marc A. Anderson ◽  
Mary J. Gieselmann ◽  
Qunyin Xu

RSC Advances ◽  
2018 ◽  
Vol 8 (24) ◽  
pp. 13567-13577 ◽  
Author(s):  
Yang Liu ◽  
Weiya Zhu ◽  
Kang Guan ◽  
Cheng Peng ◽  
Jianqing Wu

The traditional dip-coating method for preparation of ceramic membranes requires a long drying time and easily produces drying defects. In this work, an improved dip-coating process was proposed.


2015 ◽  
Vol 1102 ◽  
pp. 91-94
Author(s):  
Mohammed Nasir Kajama ◽  
Ngozi Claribelle Nwogu ◽  
Edward Gobina

Gas permeation of hydrogen (H2) and nitrogen (N2) were obtained from 30 and 6000 nm pore diameter tubular commercial alumina ceramic membranes at 0.05 to 1.00 bar and 298 K. Flow rates of up to 3.279 and 2.296 l/min were obtained for H2and N2respectively. The ratio of H2/N2flow rates were used to calculate H2/N2selectivity. The experimental H2/N2selectivities obtained were 1.85 and 1.43 for the 30 and 6000 nm respectively.


2008 ◽  
Vol 8 (3-4) ◽  
pp. 451-454 ◽  
Author(s):  
A. Kirchner ◽  
I.W.M. Brown ◽  
M.E. Bowden ◽  
T. Kemmitt ◽  
G. Smith

2017 ◽  
Vol 696 ◽  
pp. 1080-1089 ◽  
Author(s):  
Elisa Mercadelli ◽  
Antonino Salvatore Aricò ◽  
Angela Gondolini ◽  
Stefania Siracusano ◽  
Marco Ferraro ◽  
...  

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